Page 336 - Petroleum and Gas Field Processing

Sheet 11 Figure in Contactor to Gas H 2 O þ Gas Saturate to Water Feed TEG 1.0000 0.9999 0.5420 0.0000 29.44 29.44* 277.1 48.89* 62.05 62.05 62.05 62.05* 498.5 498.6 0.4990* 3.649* 9191. 9192. 8.989 512.0 27.59 27.59 0.009007 0.4543 1.021eþ07 1.021eþ07 2.961eþ04 6.562eþ05 Bttms Regen TEG LP TEG Rich Gas Dry 0.0000 0.0362 0.0000 1.0000 204.4 35.51 30.17 31.14 1.034 1.793 62.05 62.05 3.648 4.270 4.270 497.9 511.9 525.6
Flow

for Gas Out L/R

Balance Inlet 1.0000 29.44* 62.05* 498.1* 9183. 27.58 1.018eþ07 Water 0.0000 29.44 62.05 0.06651 1.200 0.001203 4527. from Lean 0.0000 145.1 1.027 3.648 511.9 0.4542 6.283eþ05

Energy (C) (bar) (C) (bar) (C) (bar)

and (kgmole/h) (kg/h) (m 3 /h) (kcal/h) (kgmole/h) (kg/h) (m 3 /h) (kcal/h) (kgmole/h) (kg/h) (m 3 /h) (kcal/h)

Material Flow Flow Flow

Stream Fraction Volume Fraction Volume Fraction Volume

3 Temperature Flow Flow Flow Temperature Flow Flow Flow Temperature Flow Flow Flow Copyright 2003 by Marcel Dekker, Inc. All Rights Reserved.
Table Name Vapour Pressure Molar Mass Liquid Heat Name Vapour Pressure Molar Mass Liquid Heat Name Vapour Pressure Molar Mass Liquid Heat